Method for separating copper, arsenic and nickel and purifying copper electrolyte
A technology of copper electrolyte and electrolyte, which is applied in the field of separation and purification of arsenic, copper and nickel to achieve the effect of simple process, low cost and reduction of black copper powder
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Embodiment 1
[0018] Take 1.6L of copper electrolyte, its composition is shown in Table 1, Pb-Ag alloy is used as anode, copper starting plate is used as cathode, and the current density is 200A m -2 , copper electrolyte temperature is 55 ℃, add bone glue, gelatin and thiourea. When Cu in the copper electrolyte 2+ When the concentration drops to 25.4g / L, adjust the current density to 100A m -2 Electrowinning copper removal to Cu 2+ The concentration is 0.42g / L. The current density is 200A·m -2 The obtained cathode copper copper content is 99.96%, and the arsenic content is 0.000602%. The current density is 100A·m -2 47.62g of cathode product was obtained. The copper content in the product was 81.43%, and the arsenic content was 6.17%.
[0019] Sulfur dioxide was introduced into the solution after electrowinning copper removal, and the flow rate was 400 mL·min -1 , the reaction time is 4h, and the reaction temperature is 30°C. The reduced solution was evaporated and concentrated by h...
Embodiment 2
[0031] Take 1.6L of copper electrolyte, its composition is shown in Table 5, use an insoluble anode, the copper starting plate is the cathode, and the current density is 180A m -2 , copper electrolyte temperature is 65 ℃. When Cu in the copper electrolyte 2+ When the concentration drops to 24g / L, adjust the current density to 80A m -2 Electrowinning copper removal to Cu 2+ The concentration is 0.25g / L. The current density is 180A·m -2 The copper content of the obtained cathode was 99.27% and the arsenic content was 0.0014%. The current density is 80A·m -2 45.9g of cathode product was obtained, in which the copper content was 81.6%, and the arsenic content was 5.98%.
[0032] Sulfur dioxide was introduced into the solution after electrowinning copper removal, and the flow rate was 500 mL·min -1 , the reaction time is 2h, and the reaction temperature is 60°C. The reduced solution was evaporated and concentrated by heating, cooled to -25°C and then filtered. The composi...
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